Apparatus and method for conducting ionic exchange operations



Dec. 19, 1944. I R. w. sHAFoR 2,365,221

APPARATUS AND METHOD FOR CONDUCTING IONIC EXCHANGE OPERATIONS Filed Feb. 28, 1942 7 sheets-sheet 1 33 l sz i a/ "M i 3 .a7 L 3.

a V- /a l l l /7 /6 /7 /726 I /Z /e 5,0 52 33a 1 @f 'g "e il. L MQ/ T... -"gli I \/.9 l l lm l1-- /4 i l1 3a I l Z, i 22; o i ,a5 5a 45 46 REaE/vfRANT-f ||l Jz//cE-v I 37 e 44 42 .INVENTOR 125 RALPH w. SHAFOR BY WHTER ge -f www 39 40 ATTORNEY R, w. SHA1-'OR 2,365,221

APPARATUS AND METHOD FOR CONDUCTING IONIG EXCHANGE PERATIONS lDec. 19, 1944.

Filed Feb. 28, 1942 7 Sheets-Sheet 2 lNVENToR RALPH w. sHAFoR ATTORNEY Dec. 19, 1944. R, w, SHAFOR 2,365,221

APPARATUS AND METHOD FOR CONDUCTING IONIC EXCHANGE OPERATIONS Filed Feb. 28, 1942 '7 Sheets-Sheet 5 INVENTOR RALPH W. SHAFOR Y n E r.

ATTORNEY APPARATUS ANDVMETHOD FOR CONDUCTING IONIC EXCHANGE OPERATIONS '7 Sheets-Shea?I 4 R. W. SHAFOR Filed Feb. 28, 1942 Dec. 19, 1944.

ATTORNEY INVENTOR RALPH W. SHAFOR 'lift il! R. W. SHAFOR Dec. 19, 1944.

APPARATUS AND METHOD FOR CONDUCTING IONIC EXCHANGE OPERATIONS Filed Feb. 28. 1 .942 '7 Shee-S-Sheekl 5 l Il .INVENTOR I RALPH W. SHAFOR ATTORNEY R. W. vSHAFOR Dec. 19,1944,

APPARATUS AND METHOD FOR CONDUCTING IONIC EXCHANGE OPERATIONS Filed Feb. 28, 1942 '7 SheebS-Sheefl 6 INVENToR RALPH w. sHAFoR ATTORNEY Dec. 19, 1944. R. w. sHAFoR 2,365,221

APPARATUS AND METHOD FOR CONDUCTING IONIG EXCHANGE OPERATIONS Filed Feb. 28, 1942 '7 sheets-sheet 7 ATTORNEY Patented Dec. 19, 1944 APPARATUS AND METHOD Fon CONDUCT- ING loNIC EXCHANGE OPERATIONS Ralph w. snafor, New York, N. Y., assignor'to The Dorr Company, Inc., New York, N. Y., a corporation of Delaware Application February28. 1942, Serial No. 432,898

20 Claims.

This invention relates to the treatment of solutions by means of ionic exchangers. More specifically, this relates to improvements in method and apparatus for conducting the operating cycle of a bed or a series of beds of exchanger material.

An ionic exchanger is usually represented in the form of av unit or cell containing a bed of the exchanger material proper which is usually granular. An exchanger has the ability to take up from the solution an ion of an ionized solute and to give oil into the solution in exchange an ion of another kind of like electric charge. Therefore, cation exchangers as a class exchange positively charged ions, whereas anion exchangers as a class exchange negatively charged ions.

As the solution is passed through and contacted with the ion exchanger bed, the direct; exchange of respective ions between the solution and the exchanger continues until the exchanger is saturated with absorbed ions to be removed and its exchange capacity thus exhausted. The exchange capacity can then be restored by treatment of the exchanger with a suitable regenerant solution. The saturation on the one hand, and the regeneration on the other hand,. represent the main phases of the operating cycle of an exchanger, whereby the exchanger may be used over and over again. The chemical reactions involved in the operating cycle are reversible equilibrium reactions. I

While this invention is broadly applicable to the ionic exchange treatment of solutions in general, it has features of particular importance for the purification treatment of sugar juices, whereby ionic impurities or dissolved salts are subtracted from the juice, the presence of which impurities otherwise would prevent a certain amount of sucrose from crystallizing and thus cause its loss in the form of molasses. Therefore, although in no limiting sense, the invention will hereinafter be described with reference to the -treatment of sugar juices.

That is to say, recent developments in the purication of sugar juice are bases upon the removal of ionic impurities or salts fronithe juice by way of ionic exchange treatment and by means of granular exchanger materials of organic nature. The se exchanger materials are known as organolites in distinction from the so-called vzeolites which are inorganic and the use of which is known and established in water purication treatment for which various types of industrial` apparatus have been evolved. A practical oper- (Cl. 21o-24) ating cycle in the purification of sugar juice by means of organolites may comprise:

1. Passing the juice to be treatedthrough a fresh exchanger bed in submergence until the bed has become saturated.

2. Displacing the residual juice downwardly from the bed by means'of wash Water. l

'3. Washing upward to displace solid phase impurities from the bed.

4. Passing regenerant solution downwardly through thebed in submergence, until the bed has become regenerated. v y

5. Di'splacing the residual regenerant solution downwardly from the bed by means of wash water, whereupon the bed is ready for a new cycle.

It is to be noted that the organolites are substantially stable in the presence of acids or alkalies, whereas the zeolites are not. This quality of the organolites is important because in the exchange treatment of the sugar juice both an acid and alkaline phase or environment are being encountered due to the particularA exchange mechanism involved (and hereinafter described). Zeolites on the other hand, are unstable unless they operate in a substantially neutral medium, as in the practice of water puriiication treatment. Another differentiating fac-4 tor never encountered in water treatment, is that 'sugar solutions or juices carry a solute (namely, sucrose) of value that involves side reactions. such as inversion of the sucrose, as the sucrose tends to deteriorate into invert sugars when unduly detained in an acid environment. That is to say, under such conditions a quantity of sucrose that is potentially crystallizable, will turn linto inert sugar that is non-crystallizable and as such constitutes a loss in the form of molasses.

It is one of the aspects of this invention that this coincidental chemical reaction of inversion be minimizedfby minimizing the time of detention of the juice in the exchanger bed, while in its acid phase.

The objects of this invention are concerned with increasing the effectiveness and the efficiency of the operating cycle of exchanger beds. This includes (a) emcient utilization of the exchange capacity proper of the exchanger material in the bed, and (b) the economic handling of the solutions or liquids being contacted with the bed, and (c) expediting the performance of the operating cycle of an exchanger cell.

One problem is how to maintain the exchanger bed free of deposits or-solid phase impurities Aattach themselves to the granules.

such as may either coat or envelope the exchanger particles or may accumulate in the interstices or voids between the particles of the bed. For instance, sugar juice to be treated by the exchanger may carry such matter or else substances which are adapted to form precipitates. Such solid phase impurities may lodge in the interstices of the exchanger bed or may A quantity of solid phase impurities may be in the form of precipitates resulting from the reactions accompanying the exchange operation.

Hence it is one object to maintain the exchanger bed free and well-washed of solid phase and freed of various kinds of solid phase impurities or deposits, the exchanger bed should be kept as of uniform depth and of uniform ow resistance throughout its area, and should be uniformly permeable with respect to the liquid or solution being passed therethrough in a downward ow. It should be understood that solutions undergoing ionic exchange in the exchanger bed should be passed downwardly therethrough for the sake of intimate and eiective contact with the exchanger material, and while the bed occupies a minimum volume.

Objects of maintaining high efficiency, as above defined, of the exchanger bed, are attained by passing through the bed an evenly distributed upward iiow of wash liquid in` such a. manner that substantially the entire range of sizes of the particles constituting the bed is placed in a sustained condition ofv suspension. This is usually known, and herein termed, as a teeter condition or true the spent teeter liquid that is being withdrawn at the top of the cell.

The provision of the extra cell space or free board above the settled exchanger bed for the purpose of teeter washing, and requirements regarding the economical and expeditious performance of the operating cycle as a whole, involve a further problem, namely, that of maintaining a suitable liquid or solution level in the cell. That is to say, the liquid level should not be allowed to fall to a point where it exposes any portion of the exchanger material, nor should it rise suciently to accumulate any appreciable amount of liquid or solution above the exchanger bed, while there is a downward iiow through the bed. By preventing an undue drop of the liquid level and thus preventing exposure of the bed, air is prevented from getting locked in the voids of the bed and from increasing the flow resistance of the bed, and also from reducing the effectiveness and exchange capacity of the bed. Accumulation of a volume of excess liquid or solution 'above the bed may be the cause of a reduction teeter condition. This requires a uniformly distributed and uniform upward ow of certain intensity of liquid through the bed, with the result that the depth of the bed expands until all the particles of theV bed are in equilibrium with the up-ilowing wash liquid. In that condition the particles range themselves-in` strata according to size with the coarsest at the bottom and the nest at the top. At the same time the particles being in some sort of an unstable equilibrium although suspended, constantly migrate around each other in the various zones or strata. This not only flushes out the loose matter between the particles, but it also produces a certain amount of gentle contacting between the particles, whereby solid phase impurities or precipitates that are clinging to the particles are effectively loosened up and carried away by the upward flow-of the wash liquid, to be withdrawn at the top of the exchanger cll. When the upflow is stopped, the particles in teeter settle down or subside and come to rest in strata according to sizes, with the coarsest at the bottom and the finest at the I()lonsequently, the cell construction according to this invention provides for a predeterminable amount of extra cell space of free board above the top strata of the settled bed, to allow for-the expansion of the exchanger bed when in teeter as above described. The freejboard also includes an upper margin or extra depth of liquid above the top strata of the teeter bed. to insure that novparticles from the top'are carried away with -in total operating eiiiciency of the operating cycle of the bed. Accumulation of excess liquid or solution above the exchanger bed may mean any one ofthe following objectionable conditions: that sugar juice accumulates above the bed while in its -acid phase, which is the same as saying that its detention time in the acid phase is increased with the accompanying deteriorating effects due to inversion, that a correspondingA excessive amount of Water is needed for downward displacement of the juice, and that, moreover, the juice becomes unnecessarily diluted; or it may mean that an undesirable excess volume of regenerantsolution builds up above the bed, again requiring a corresponding excess of wash water for downward displacement and at the same time effecting undesired dilution of the regenerant solution.

Taking sugar juice for example, undue fluctuations of the liquid level in the exchanger cell may be due to the following reasons: in treating sugar juice in a series of exchanger beds, the juice in one bed due to ilow resistance in the subsequent beds,-may rise unduly above the top strata of the exchanger bed, compressing the air above the liquid, thus creating an accumulated or dead volume of juice above the bed, and unduly in'- creasing the detention time of the juice. On the vother hand, with closed type tanks containing exposing emerged exchanger material and reducing the effectiveness or capacity of the exchanger bed. Air or gas may be entrapped in the feed juice, or gas may form in the juice due to side reactions, while undergoing ionic exchange. Gas or air or both collecting above the juice level in the cell may cause fluctuations of the juice level.

Therefore, it is another object of this invention to provide means whereby the liquid or solution level in the exchanger cell can be controlled, and be maintained above, although close to, the top strata of the exchanger bed, in other words, whereby the excess liquid volume above the exchanger bed can be kept at a minimum.

can be allowed to rise or be depressed co spondingly.

According to one feature this control is effected by varyingthe pressure of a gaseous medium in the space above the liquid level. For instance compressed air may be introduced into, or be released from the cell. The action of the compressed air in the space above the liquid level may be compared with the action of a piston, with' the cell representing the cylinder in which it operates to control the liquid level. This variable air pressure cushion is therefore herein alternatively termed an air piston.

Ac'cording to another feature such control is automatically effected in response to the juice level rising above, or falling below a predetermined limit, and it is herein termed automatic level control. f

More specifically, control means are provided comprising photoelectric devices responsive to predetermined or critical limit positions of the juice level, whereby either pressure from the tank is released, or compressed air is admitted into the tank, as the case may be, in order to maintain the juice level adjusted between the upper and lower predetermined limits.

According to another embodiment, automatic means for effecting this pressure control coinprise float controlled devices responsive to fluctuations of the juice level whereby pressure can be released from the tank, or else air pressure be introduced into the tank.

Other features reside in floating baffle means whereby feed liquid impinging upon the top of the bed is intercepted and distributed. By thus maintaining a level top strata of the bed there is maintained uniform effective depth and consequently uniform flow resistance and uniform effectiveness of the bed throughout. These bale means are in the form of a perforated floating baffle plate sustained by the liquid level above the bed or resting upon the bed.`

This baffle plate while protecting the top strata l of the exchanger bed against disturbance from impinging feed liquid also acts as a displacement member, in that it occupies a portion of the liquid above the top strata of the settled exchanger bed, thereby reducing the effective excess volume of liquid above the bed. The baille plate floats upwardly with the rising liquid level and thereby permits the unhampered expansion of the bed during the teetering phase thereof. The upward floating baille plate is arrested within a margin of liquid to be maintained above the teether bed proper, and will then serve to absorb ow disturbances that might react into the teeter bed due to the withdrawal of liquid at the top.

lAccording to another feature there is provided in this exchanger cell a central feed inlet and spray valve from which feed liquid or solution issues under pressure, being projected on to areas or zones concentric with the Valve at the top of the exchanger bed.

More precisely, there is provided in the cell a central feed inlet conduit rising from the bottom portion of the cell and surrounded by the exchanger material, which inlet conduit terminates in a weighted valve through which the feed inlet under pressure is distributed over the top area of the exchanger bed. The exchanger bed surrounding the inlet conduit thus forms an unbroken and unobstructed mass, and may be maintained as such as of uniform depth and of uniform flow resistance therethrough.

Other features have to do with the mounting of the inlet conduit in the bottom portion of the exchanger cell.

Still other features provide means and a method of operating them, for effecting the up-flow washing of the exchanger bed, by teetering. Such means comprise a perforated plate, herein called constriction plate, upon which the exchanger material is supported, and which is constructed and operated in a manner to produce uniform up-iiow of wash water throughout the area of the bed and at a rate to induce a true teeter condition in the bed, with the result that cloggings in the bed are broken up and a mobilized condition of all particles is established. A characteristic of such a true teeter bed is size stratification of the exchanger particles, which stratification is being maintained due to the sustainedand uniformly distributed up-flow of the wash liquid through the teeter bed, while excess wash liquid is withdrawn at the top. Due to the size stratification of the exchanger grains, the holes in the constriction plate that sustains the bed, need not be largerthan is necessary to prevent the passage therethrough of the coarsest fraction of the grains that constitute the bottom strata of the exchanger bed, while the number and distribution of the holes should be such as to make it possibl to induce the up-fiow teeter condition set forth. f

The invention possesses other objects and fea-y tures of advantage, some of which, with the foregoing, will beset forth in the following description. In the following description and in the claims, parts will be identified by specific names for convenience, but they are intended to be as generic in their application to similar parts as the art will permit. In the accompanying drawings there has been illustrated the best embodiments of the invention known to me, but such embodiments .are to be regarded as typical only of -other possible embodiments, and the invention is not to be limited thereto.

The novel features considered characteristic of my invention are set forth with particularity in the appended claims. The invention itself, however, both as to its organization and its method of operation, together with additional objects and advantages thereof, will best be understood from the following description of a specific embodiment when read in connection with the accompanying drawings in which:

Fig. 1 is a part sectional side view of the exchanger unit or cell. y

Figs. 2, 3 and 4 are cross-sections taken upon Fig. 1 along the lines 2-2, 3-3 and 4 4 respectively, to show details of the mounting of the constriction plate at the bottom of the tank, andk sent vertical detail sections along the lines 5 5 of the photoelectric conthat the control is effected by meansof float devices.

Figs. 8 to 13 are diagrammatic views illustrating various phases of the operating cycle of the unit.

Figs. 14 and 15 are diagrammatic illustrations of the method for effecting and maintaining a bed of exchanger material in which the particles or granules are stratified according to size.

Figs. 16, 1x7 and 18 are detail views showing a lower limit position, a normal or mean position, and an upper limit position of the liquid level above the exchanger bed and corresponding positions of the iioating baille member.

Inasmuch as the ionic purication treatment of sugar juices is herein chosen as an example of embodying this invention, and so. that the environment of the invention thus embodied may be clearly understood, there now follows a brief description of the chemical exchange mechanism whereby ionic impurities or dissolved salts in the sugar juice are subtracted therefrom and replaced with the molar equivalent of pure and evaporable water.

In extracting non-sugars and especially salts from sugar-making juice or syrup, two main types of exchanger beds are used. One is called the cation exchanger bed that ischaracterized by its use of exchanger material that operates on the hydrogen-ion cycle and is adapted to collect from the juice plus or positively charged ions represented generally by calcium, magnesium, sodium and potassium. That is, as juice is supplied to the cation exchanger bed (or cell that contains the bed) so as to iiow through it and out therefrom, cations of the juice exchange themselves for the hydrogen ions of the exchanger until the exchanger bed becomes exhausted of its exchange capacity and so saturated with those cations that it ceases substantially to exercise further exchange activity. Thereupon the cation bed must be regenerated by contact with a regenerant in the form of an ionized strong acid such as hydrochloric or sulphuric acids. During regeneration, the reverse process takes place in the exchanger, namely, the residual cations exchange with hydrogen ions of the acid regenerant so that the cations flow from the bed until the bed is completely recharged with hydrogen ions Juice that passes from the cation bed has had its'impurity content of basic ions substantially removed, but it yet contains chlorides, sulphates and other such negative ionic impurities. So the `juice substantially rid of its positive ionic or cation impurities, that have been left in the exchanger, is passed to and through an ion exchanger bed or cell that operates in a hydroxyl cycle. In passing through the anion bed, the chloride and sulphate, etc. ions of the juice are exchanged for the hydroxyl ions of the bed until the anion bed becomes saturated with chlorides and sulphates, etc. Thereupon the saturated moved from it while passing through a subsequent anion exchanger bed.

The exhaustion of a fresh exchanger bed, while the solution is ilowing downwardly therethrough, proceeds in continuous fashion from the top to the bottom of the exchanger body. Hence, there exists a dividing line or zone of transition between the upper exhausted portion of the exchanger body and the lower non-exhausted portion of that body. This dividing line or zone keeps shifting downwardly through the exchanger body as the continuously through-flowing solution leaves an increasing exhausted exchanger portion behind while advancing through a correspondingly decreasing portion of non-exhausted or still-active exchanger. Since the dividing'line is not necessarily a sharp one, there will be noticed a slowing down of the exchange intensity as the bottom of the exchanger bed is being approached. This is indicated by a corresponding rising of the pH of the solution leaving the exchanger, and it is a warning that a fresh or regenerated exchanger should be substituted for the one nearing exhaustion. The regeneration of an exchanger bed proceeds in a similar manner progressively through the bed.

In the course of a complete operating cycle, each of these exchangers if exhausted, is to have the residual juice therein displaced from the exchanger bed with wash water, and if deposits have collected on the exchanger granules they are to be washed out, before the exchanger is subjected to contact with the regenerant solution. Again, if regeneration is completed, the residual regenerant is to be displaced and Washed out from the exchanger with water, before the exchanger is again contacted with the juice. In this way undesirable reactions between ionic consti'tuents of the juice and regenerant solution in the exchanger bed can be avoided and the exchanger be kept in regular cyclic operation with substantially undirninished efliciency.

It is further to be noted that the cation and anion exchanger materials to be used in the treatment of sugar juice as herein exemplified, must be stable in the presence of acids and alkalis respectively, that is, they must be resistant to disintegration in such enviromnents and substantially retain their granular condition. An example for a suitable cation exchanger for that purpose is the cation exchanger furnished by the anion bed must be regenerated by contact, with` some ionized alkali hydroxide or carbonate, espe-f cially sodium hydroxide or carbonate. During regeneration, the reverse process takes place, 1

namely, the residual chloride and sulphate. etc. ions in the bed exchange with hydroxyl ions of the basic regenerant so that the negative ions or anions flow from the bed until the anion bed is In passing Resinous Products Company of Philadelphia, under the name or identification of Amberlite IRl. A suitable anion exchanger is furnished by the same source under the name or identication of Amberlite IR 4. These are exchanger materials of synthetic resinous nature. and more specically materials which are preparedby the condensation of a dissolved organic chemical of a group comprising sulfonated phenols and aro matic amines with an aldehyde.

From the Vforegoing description of the exchange operation involving the puriiication treatment of sugar juice, it Will be understood that the juice, in passing through a cation and anion exchanger station, is temporarily acidied. That l is to say, it passes through an acid phase in which it is first increasingly acidiiied because of acidity induced by the operation of the cation exchanger, and then again gradually deacidiiled because of the action of the anion exchanger in which the previously induced acid. is replaced with pure water.

Since an acid environment in the juice promotes inversion of the sucrose, it becomes desirchanger cell close'to the top surface ofthe exchanger bed. On the other hand, the juice level must not drop so far as .to expose by emergence the top portion or top strata ofthe bed. According to this invention, air or gas pressure in the exchanger cell upon the liquid level above the bed is controlled so as to maintain the juicelevel at a desired elevation, that is to say, close enough to, but not too close,to, the top of the exchanger bed.

The exchanger unit or cell constructed according to this invention comprises a cylindrical upright tank I9, having. a cylindrical body portion provided with supporting brackets Il,

' a top cover portion I2 closing the upper end of the cylindrical portion and fastened thereto vas by means of a bolt and flange connection I3, having a gasket |33, further having a bottom portion 4 that closes the lower end of the cylindrical body portion and is fastened thereto means of a flange and bolt connection I5, gaskets being indicated at |511. Interposed between the lower end of the cylindrical portion and the bottom portion I4 is a perforated plate I6 herein called constriction plate, that sustains the load of the granular exchanger material forming the exchanger bed in the cell bed which is herein designated by its-depth D. The constriction plate I6 is confined at its upper as well as at its underside by a system of ribs, that are provided on a body portion of the tank on the one hand, and on the bottom portion |4 on the other hand. The arrangement of which ribs or reinforcements may be seen more clearly from cross sectional views in Figures 3 and 4, and also in Figure where the parts are drawn apart.

That is to say, the lower end of the body portion I I is provided with a system of annular concentric ribs I1 intersected by radial ribs I8. The bottom portion I4 has concentric ribs I9 shown to match the concentric ribs 1 above.` The bottom portion I4 of the cell is slightly conical and is shown to have an outer skirt portion having the identical diameter as the cylindrical body portion I I of the cell, and also to have four radial channels 2| leading into a central well 22. Through this central well 22 and continuing upwardly into the interior of the cell extends a feed induction pipe or feed. conduit 23 which is held in place by means of a flange 25 that is unitary with the feed induction pipe and in turn fastened by'means of flange and bolt connection 25a and a gasket 25b to the bottom end of the central well 22. The feed induction pipe `turn is unitary with the feed induction pipe 23 and fits the seat 26 when the induction rpi'pe is mounted in place. The relationship of the parts suchas the. body-,portion with system ofy ship of all these parts withrespect to one another appears more clearly from Figure 5,' where the parts' are drawn apart.

The feed induction pipe or conduit 23 -is shown 'to extend about half way up the interiors: the

cell and to terminate at a point somewhat above the top strata of the bed D of exchanger material when in settled condition. The upper terminal portion of the'feed induction pipe 23 is provided with an induction valve. 28, comprisl ing a Avalve body 29 and a valve seat 29",v therefor, the valve body being suitably weighted down upon its seat.l The vsolutionpassing through the feed induction pipe upwardly under suitable pressure will lift the valve body 29 sufficiently from its seat to permit the feed'liquid to be' projectedl in trajectories from the induction valve 28 to annular zones concentric with the valve at the top of the exchanger bed. 'Ihe lift of the valve body 29 is limited by adepending cylindrical member 28a the upper end of which is fastened to the top cover portion I2 of the cell. Liquid introduced in this manner through the induction valve, flowing down through the depth D of the bed and passing through the perforations I6 in the constriction plate I6, collects in the central well 2 2 by way of the radial channels 2|, and leaves the Well and the exchanger unit as a whole by way of a radial pipe 30. This pipe serves as a discharge pipe for liquid being treated, or else for spent regenerant solution having passed downwardly through the exchanger bed, but it may also serve as an in-leading connec- 40 tion for a reverse now, that is, for wash water to be introduced from the bottom to i'low upward- 1y through the exchanger bed, an operating phase hereinafter more fully to be described. From the radial pipe 30 the outflowing liquid may be allowed to pass upwardly through one of a num.- ber of risers or goosenecks or spigots 3|, 32, 33, the point of overflow from which is placed high enough to normally keep the exchanger mater'ial in the bed in submergence.

In order to conduct a desired operating cycle (such as hereinafter described), there are further provided the following pipe connections and valves: A header 34 into' which leads a connection for regenerant solution having a valve 36, an inlet connection 31 for the liquid or solution such as sugar juice to be treated, a valve 38 for that connection, a water inlet connection 39 having a valve 40, and a 'water by-pass connection 4| having a valve 42 that permits shunting the water inlet from the header 33 to the radial pifpe 30. lThe header 34 is provided with a valve 43 disposed intermediate regenerantv inlet connection 35 and the juice inlet connection `31, and lfurther provided with a'. valve M disposed intermediate juice inlet connection 31 and the water inlet connection 39. The radial pipe 30 has a shutoif valve 45 to be closed when wash water is to be introduced through that pipe from the bypass connection 4I into the bottom of the exchanger bed.A The risers 3|, 32, 33 have corresponding shutoff valve 3|, 32a, 33B. It will be further seen that the radial pipe 36 connects with a header 46 from which rise the aforementioned risers 3|, 32, 33 and from which also leads a pipe connection 41 provided with a shutoi valve 4I through which liquid or solution that has been treated inthe exchanger bed of the cell,'can be continued forvfurther treatmentsuch ad in Vanother exchanger unit or cell.

When in the course of the operating cycle the bed oiexchangerv material in the cell is to be washed `in order to flush out therefrom solid pbase impurities or the like, wash liquid or water can be introduced under rpressure through the radial pipe 30 by opening the valves 4I) and 42 and closing all other valves so far enumerated.

From the radial pipe 30 the wash water passes into the central well 22 and then by way of the radial channels 2| to allpoints of the constriction plate I6 and through the holesA i6* thereof, upward the total effective height H of the interior of the cell, namely up to a point of overflow as represented by the overilow edge of a. launder 49 that extends inside the cell and 'circumferentially along the upper end portion '.tliereofiA The wash liquid rises until it overilows fintothis launder from which it leaves the yexchanger cell or unit through a discharge pipe 50 and a valve 50a.

Normally, when the liquid; from the induction valve 28 ilows downwardly through the exchangerobject of this 'invention' (and by means here.V

the lower linut level La. In this respect reference may be had to Figure 1 and Figure 6.

The principle relied upon to eiect the desired liquid level control, is embodied in a pair of photoelectric devices to maintain the liquid level between the forementioned upper and lower limits, by releasing gas or air pressure above the level so as to permit the same to rise from its lower limit, or by introducing into the cell gas or air pressure whereby to depress. the liquid level from its upper limit position. 'I'hat is to say, one of the photoelectric devices will respond, when the lower limit level is reached, by causing through relay effect Vthe release of air or gas pressure from the inbed, there is to be maintained accordngfto the inafter tojbe described) an' average or mean solution level L' that is slightly above the top level Y. oi" the material'of theexchanger bed and preferably just suilicient to keep the material in submergence and thereby to keep the dead volume of liquid above the exchanger material at a minimum. The maintenance of an average 3 level L is effected by certain control means whereby it can be either manually adjusted, or automatically controlled between an upper limit level L1 and a lower limit level L2. In Figure 1 the mean liquid level L is shown to support a floating annular perforated baille plate 5| that is thus oatingly sustained in the solution above thebed close tothe top strata thereof.

When the flow of liquid through the exchanger bed is reversed, namely when passing wash liquid upwardly therethrough during the wash or teetering phase of the operating cycle, the iloating baille 5| will rise with the rising level of the upilowing liquid as the material of the bed is gradually being thrown into suspension or so-called teeter.

The height ofthe cell and the upflow rate of the wash liquid are suilicient to permit a desired teeter condition of the particles to establish itself without permitting the particles to reach the overow from the cell. The upi'loating baille is incidentally arrested as it engages the underside of the launder 49 (see dot and dash line position of the baille in Figure 1). Excesswash liquid that continues to rise through and to sustain the desired teeter bed, will pass through the perforation 5l of the baille plate 5l, will overflow into the launder 49 and leave the cell through the discharge pipe 50 and valve 50S.

Near its bottom the exchanger cell is provided with a drain connection 52 having a drain cock or valve 53. A manhole connection 54 is provided terior of the cell, whereas the other photo-electric device responds when the upper limit level is reached, by causing through relay eiect the introduction of air or gas pressure into the interior of the cell. In this way the co-actlon of the two photo-electric devices will automatically maintain the liquid level within pre-determined upper and lower limits and thereby will keep to a minimum the undesirable dead volume of solution or sugar juice above the exchanger material proper. The two photo-electric devices will now be described by reference to numbers as follows {whereby reference is made more particularly to Figure 6 including the detail sections 5-5 and 5'-'5 thereof). About midway between its top and bottom the exchanger cell or unit is shown to have provided at each side thereof a liquid level indicator casing 51 and 58 respectively. Each casing communicates with the interior of the cell by way of a lower opening and an upper opening, covered by a suitable liquid permeable member 58a of screen material or wire mesh whereby granules of the exchanger material are kept out of the casings 51 and 58 respectively. The bottom of each casing 51 and 58 has a drain or clean-out connection shown in the form of drain cocks 58, whereby exchanger particles that may have penetrated the screens 58 and 58b can be removed or flushed out. Each casing has a transparent portion in the form of windows 59 and 60 respectively on opposite sides of the casing, so that a light ray sent through the transparent portion of the casing is either allowed to pass therethrough or is arrested or obscured, depending upon whether or not liquid iluctuating in the casing intervenes or does not intervene in the path of the light ray, since the casing has hydraulic communication with the liquid in the cell. That is to say, the liquid such as sugar juice may obscure the light ray, and the photo-electric device may be so adjusted as to send out a control impulse in response to the obscuring of the light ray. Conversely the device may be so adjusted as to be inactive while the light ray is obscured, but to send out a control impulse when the light ray is free to pass through the transparent portion of the corresponding indicator casing or chamber. The transparent portion of the indicatoi` chamber 51 is interposed in the path of a light ray of a photo-electric device 6i whereas the other indicator chamber 58 is interposed in the path of a light ray of another photo-electric device 62 with the addition of swingable cover portions lila and 62a respectively. Each of the photo-electric devices is vertically adjustable as indicated by vertical spindles Gib and 6212. Figure 2 shows these photo-electric devices in plan view, whereas Figure 6 includes detail sections 5-5 and 5-5 of the respective photo-electric devices, from which their disposition and function can be more clearly understood. Referring more particularly tu Figure s, the' photo-electric device 6l comprises a light source' unit 68 at one side of the indicator casing 51 and a light responsiveA sponsive relay unit 66 at the opposite side of the indicator casing 58. The photo-electric device 8| is so positioned and adjusted that it will remain inactive or nonresponsive as long as liquid in the indicator casing 51 stands high enough to obscure or interfere with the passage of a light ray 51' therethrough from the light source unit 63. This is the case whenthe liquid level is above its lowei` limit La and for instance at its intermediate level L. If due to a change in the pressure conditions in the interior of the cell, the level drops to its lower limit position, the light ray emanating from the light source unit 63 will pass through the transparent portion of the indicator casing 51 and strike the light responsive relay unit 64 causing the same to set up a relay circuit whereby a solenoid controlled relief valve 61 is opened and interior pressure from a gaseous medium such as air in the cell is released through opening 68 in the member 28B, and by way of pipe connections 68, 69, 18. A hand operated vent cock 18* is shown to be provided in the cover portion' l2 of the tank. A partition wall 68h in the hollow member 28B is shown slopingl down towards the lower edge portion of the openingr 68. This permits the liquid level to rise as the introduction of feed liquid to the cell continues, and in rising the liquid again obscures the light ray 51a through the indicator casing 51 thereby interrupting the relay circuit and consequently deenergizing the solenoid of the relief valve 61, allowing the same to close. The new liquid level thus established is intermediate the predetermined upper and lower limits, and will remain so as long as no further undue pressure fluctuations occur inthe interior of the cell.

The other photo-electric device 62 operates similarly in that it responds to a rise of the liquid levelto the upper limit L1. That is to say, the photo-electric device 62 is so positioned and adjusted with respect to its associated indicator cas'ng 58, that normally and as'lone as the liquid level remains below its upper limit `and the light responsive relay unit 66 will thereby be caused to set up a relay circuit energizing the solenoid of a solenoid controlled air pressure supply valve 1|, causing the same to open and to force compressed air from the air pressure supply pipe 12 through pipe connections 14, 68 into the interior of the cell. 'I'he sole'- noid controlled valves 61 and 1| may be such vas shown in the General Electric Co.s Industrial Control Handbook of May 1, 1939, CRI-9507 Page 5, and page 6. There is also shown a hand-controlled valve in the air pressure supply connection 14.

It will be noted that both photo-electric devices 6| and 62 are supplied by a common source -of power indicated by the two conductors 16 and 11. Branch conduits 18 and 19 llead to points 88 and 8| from where one branch circuit represented by conductors 82 and 83 feeds the light source unit 63, and vanother parallel branch circuit leading into and out of the light respon- 'l sive relay unit 64 comprising conductors 84, 85,

86, 81, which branch circuit when closed by the iight responsive unit 64 actuates the relief valve 61 by energizing the solenoid thereof. 1

Similar branch circuits supply the other photo-electric device 62 and its associated solenoid controlled air pressure supply valve 1|. That is to say from points 88 and 29 of the common source of power supply branch conductors 9|) and 9| extend to points 92 and 93 from where one branch circuit represented by conductors 94 and 95,. feeds the light source unit` 65, while another branch circuit represented by conductors 96, 91, 98, 99 when lclosed by the light responsive unit 65 energizes the solenoid of the solenoid controlled pressure supply valve 1|. \.f

From the foregoing it will be understood that; while the liquid level L in the cell remains within the space intermediate the upper and lower limits L1 and Lz, the relays ofthe photo-electric devices will remain inactive, so that the two solenoid controlled valves 61 and 1| will remain closed. When the air volume in the cell increases, as may be the case due to entrapped air enteringwith the feed liquid and collecting as an air cushion above the liquid, or because of gases forming as a result of chemical reactions incident to the ionic exchange process in the cell, suchaccumulation of a gaseous medium will depress the liquid level. Ifthe depression reaches the lower limit In it will be automatically corrected, since the photo-'electric device 6| then operates to open the relief valve 61 until a mean level L has again restored itself. Should,

on the other'hand, the level rise to reach the' air into the cell long enough to restore or depress thelevel of a mean position L. As the-liquid level in the exchanger cell varies, the iloatable Abaiile plate 5| may vary in position accordingly, as exemplified in the detail showing f of Figures 16, 17 and 18. When the level assumes the lower limit position La (see Figure 16), the bame plate is shown to be resting on top of the exchanger bed. When the level assumes the mean or normal position L (see Figure 17),

the baille plate is shown to be just about floating with only a thin stratum of liquid between it and the bed, whereas when the level assumes its upper limit iloating position L1 (see Figure I8), the liquid strata between the'bailie and the bed is accordingly somewhat deeper. three positions however, the baille pla' 5| also functions as a liquid displacing member, with the result that whatever the volume of the liquid labove the exchanger bed, that volume is reduced by the displacement ofthe floating baille 5|. This means in'eifect that corresponding exchanger cell may be controlled in such a manner that it does not fluctuate, for instance. more than three inches above, and three inches below mon junction H3* with the pipe connection HI the mean level L; in other. words, the control may be such that the upper limitz level AIn is not more than three inches above, and the lower limit level La and more than three inches below the mean level L. The position of the two limit levels in turn may be such that, for instance, the lower limit level Le is substantially not more and not less than about one-half inch above the top of the exchanger bed. This means that the level is controlled within six inches maxi- 4mum deviation and is at least one-half inch,

and at most six and one-half inches above, the top strata of the exchanger bed. Considering a bed of 6 feet depth with 60% voids between the grains of the bed, this would mean an approximate fluctuation of 7% of the time of detention of the juice in the bed. e

AS a modification, instead of the photo-electric control devices, Fig. 7 shows a, pair of float controlled devices or'valves whereby the liquid level in the exchanger cell can be similarly controlled, namely, so as' to be maintained within an upper and a lower limit by means of automatically adjusting the gas or air pressure above the level in the cell. These devices are in the nature of iioat controlled valve units and |0| respectively, the one being a relief valve ,unit and the other a pressure supply unit. The relief valve unit |00 releases excess pressure from the interior of the cell, the pressure supply valve unit |0| introduces a gaseous pressure medium, such as compressed air, into the interior of the cell.

The valve unit |00 comprises a float chamber |02 communicating with the liquid that subthat extends into the interior of the cell. The upperchamber |23 connects with an air pressurev supply pipe |26 coming from a compressed air supply header |21 and has a hand-operated shut-off valve |26. A pressure gauge |29 is provided, indicating the pressure in the interior of the cell.

It will be noted that" the pressure relief valve unit |00 operates in an opposite sense to that of the pressure supply valve unit |0|.` That is to say, whenever the liquid level drops or is depressed to a predetermined minimum La in the course of the operation of the cell, this will cause the relief valve unit |00 to open by moving the valve disk |06 downvs rdly and away from, its seat |01, thereby relieving excess pressure in the cell by allowing it to escape through the ventpipe ||4 into the atmosphere, and thereby permitting the liquid level to rise, provided theviiow of feed liquid continues normally. A falling of the level merges the exchanger bed in the cell, a, iioat member |0 in the chamber, from which a valve stem |04 extends upwardly through a gland |05. The stem |04 carries a, valve disk |06 engaging a valve seat |01 in a valve housing |08 having a gland |09 through which the valve stem |04 extends into the valve housing. The valve housing |08 mounted on the top' cover portion I2 by means of a bracket |082 has a lower chamber ||0 and an upper chamber The lower chamber ||0 connects with a pressure release pipe ||2 leading to a pipe connection H3 extending centrally throughl the top cover portion |2 into the interior of the cell. A drop of the liquid level in the cell lowers the `iioat member |03 moving the valve disk |06 downwardly from its seat |01, thereby releasing Aexcess pressurel from the interior of the cell into the upper valve chamber and through ber ||6 in the float chamber, from which a valveV stem ||1 extends upwardly through a` gland |I6. The upper end of the valve stem ||1 carries a valve disk Il!! engaging a valve seat |20 in a valve housing |2| into which housing the valve stem ||1 extends by way of a gland |22. The valve housing |2| mounted on the top cover portion I2 by means of a bracket |2|* has an upper chamber |23 and a lower chamber |24. The lower chamber |24 connects with an air pressure induction pipe |26 leading into the pipe connection H3. The pressure induction pipe |25 and the pressure release pipe I| 2 form a comwill leave the valve disk ||9`of the other valve unit |0| weighted down upon its seat 20, thus keeping the compressed air supply from the header |21 shut oil from the interior of the cell. If on the other hand, the level in the cell rises to a predetermined maximum L1, this will force the relief valve disk |06 upwardly, keeping it closed, while lifting the pressure supply `valve disk H9 upwardly from its seat |20, thereby admitting compressed air to the interior of the cell through the pressure induction pipe |25, provided the pressure supply valve |28 is open. By suitable arrangement and adjustment of both flow control valve units |00 and |0| with respect to one another and with respect to the top of the `exchanger bed, the liquid level above the exchanger bed may be controlled so as to bemaintained within an upper and a lower predetermined level above the top of the exchanger bed, with the result substantially as described in connection with the operation of the photo-electric devices previously described in connection with Figs. l and 6.

The importance of the constructional features of the exchanger cell and of the control accessories therefor, will be more clearly understood from an analysis of the operating cycle f the cell, especially where the purification treatment of sugar juice is involved.

During one portion of this cycle the sugar juice to be treated, the sWeetening-oii water and subsequently the regenerant solution and final wash water therefor, are passed in a downflow through the exchanger bed. Namely, (see Fig. l), the liquid or solution is introduced into the cell under pressure as by way of the central feed induction pipe 23 and the Weighted induction Valve 28. Accordingly the entering liquid is shown as being projected from the valve 28 in trajectories to annularzones surrounding the valve. The projected liquid is intercepted by the floating perforated baille plate 5| which helps to distribute the liquid uniformly over the area of the bed and prevents it from impinging directly upon the bed and from disturbingpitting, or eroding the surface strata thereof. In this way, there is prevented a disturbance of the uniformity of effective depth of the bed, and thereby a reduction inthe effectiveness thereof.

The liquid, solution, or sugar juice` thus introduced under pressure passes downwardly through the bed D of exchanger materiaLand through the holes I6a in the constriction plate I6, and by iiow phase of the operation the overflow discharge valve 50% atthe top ofthe cellmust be'loseiiin view of the air pressure conditions tobeniaintainedin the cell by the liquid. level Vcontrol devices such as the. photo-electric-devices or vioat controlled valve units above described@ Another phase of` thev operating `,CyclefoLthe exchanger cell comprises areverse how, that ,is, an upward flow of the teeter Wash liquidthrough the exchanger bed. In that case wash water; is

passed from the water supply pipe .39 .through valve 44l! and throughthe by-pass connection-4| by way of valve 42 into the radial pipe 30,; valves 36. 43, 38, 44 and 45, meanwhile being `closed while the valve 50% at thetop of the unit is open.

`The water passes into the central well 22. from .v

established, whereby size stratification is effected.-

This means that the `upflow conditions are such that the nest particles range .themselves'in the top strata, and `that in the downwardly succeeding strata the particles become increasingly coarse, with the coarsest size at the bottom.

The character of the teeterk condition as compared with the settled condition of the exchanger material in the bed, is illustrated in diagrammatic fashion in Figs. 14 and 15 respectively.

In Fig. 14 there is diagrammatically shown la tank |3| having spaced from .the bottom a perforated plate |32 adapted to support the bed of exchanger material |33 (see Fig. l5). IWash water is indicated by arrow |34 to enter through a valve |35 the space. |36 between the bottom |31 of the tank and the perforated plate |32, while the valve |38 of a riser orgooseneck or spigot pipe |39 is closed. Providing suitable conditions k(such as will be discussed below), the liquid flowing upwardly through the perforated plate |32 passes through the exchanger'bed at a rate whereby the granules or particles ofthe material in the bed are rst loosened up and then thrown into suspension. In this way under sustained upflow of the liquid. a teeter bed is formed in whichtie particles are free enough to move so as to classify themselves in strata as to size,

following the hydraulic law underlying this phenomenon. The finest particles are thus brought to tice top strata while the coarsest remain at the bottom. Under suitably vcontrolled flow conditions the expanded or teeter bed of particles is shown in Fig. 14 to have a depth T leaving a depth t of clear liquid above the top strata of the teeter bed. the liquid'level O being "ened by the overflow edge of an overflow launder |49 from which overflowing liquidis discharged as at |4I.

Fig. 15 contrasts with Fig. 14, in that it illustrates the condition of the granules and particles' of the exchanger bed, when the same have again subsided into a settled, even though liquid, permeable mass that is supported by the perforated plate |32. This condition, of course, develops when the upiiow of liquid is stopped and, instead,

the excess liquid allowed to drain out of the tank through the riser |39, when the valve |35 is closed and thevalve |38 is open. The particles ofthe bed then having settled downvv unauthe perforated Plate 132.v to. establish va'..bed fltlv: .death P- with' a final clearwater, levelgC djustingitself a slight ditanezd-.abovethe @strata Qf the bed. `corr-.ev spondineta theverflowtlevelof the spigot pipe or l.riser |39. Under the conditions herein assumed .to prevail, it will Vbe noted that the. lexparidad-or .teetenbed assumes adepth (see Fig. 1 4) that isherein `shownto be approximately twicethe depth Boi the bed of settled particles (infFig.`15). y

It is aconcept vkof, this invention `to include in the operating cycle a period during which a teeter bed ismaintained, to serve the rdual purpose of: (1) to enable solid phase impurities` l or deposits to be washed out thoroughly from thebed, and (2) yto cause the `particles or granules `to range themselves in strata according to size, with the finest atthe top .and the coarsest at the bottom of thebed. According to the invention the toeter condition of the bed is to be established by means of a suitableT liquidperrneable means, -and such meansare herein shown to comprise a suitably perforated retaining plate, or perforated false bottom,y or as it is hereingcalled, a constriction plate.. .The constriction plate I6 sustains the bed of granular material when the same is in settied condition. While it. is desirable to have the Iholes Hia in the constriction plate large enough to reduce' the head loss therethrough to a minimum, they should substantially not be llarger than the coarsest size particles that have ranged themselves inthe bottom strata of thebed, since no particlesvmust be allowed to fall through the holes and thereby deplete the bed of its material. That is to say,the holes should substantially be just small enough toA enable the constrictionplate to eiectively sustain the largest size particles and hence the bulk of the bed thereon. It thus appears that the size of the holes I6*i in the constriction plate may be found by determining the size of the coarsest grade particles and its proporcated by a line or lines of arrows,` making these figures atleast partly self-explanatory. The sequenoe of operating phasesis as follows:

the-valves 38' and 43, and upwardly through the feed .induction pipe 23,' and then in overcoming the pressure of Vthe induction valvebod'y 29, the juice is projected along trajectories |30 onto zones concentric with the induction valve 28. VThe juice strikes the perforated iloating baille `plate 5| whereby it sevenly distributed over the area of the bed without stirring or disturbing the top strata thereof by the impact of impingement. The juice then passes downwardly through the exchanger bed D, through the constriction plate i6, and by way of the central well 22 and through the radial pipevlil, out of the cell unit. In accordance with the ow of the juice through the unit as indicated by the arrows all valves through which the juice is not shown to pass in Fig. 8, are closed. It will also be noted that all valves and pipe connections in this diagram (as well as in the others, Figs. 9 to 13) are numbered the ysaine as corresponding ones shown in Fig. 1.

In Fig. 9 the ilow of juice down through the bed is shown to have been stopped because of the exchange capacity of the bed is now assumed t have been exhausted. The residual juice in the ,bed must be displaced with wash water before the regeneration of the bed can be undertaken. Therefore Fig. 9 shows (by means of arrows) the displacing wash water entering through the water supply pipe 39, and valves 44 and 43, through the induction pipe 23, and against the weight of the valve body 29, into the cell. Due to the pressure it projects in trajectories to zones concentric wtih the induction valve 28. It passes through the perforations of the baille plate downwardly through the bed, through the constriction plate I6, the well 22, the valves Sand 3i, and again up the yriser 3i whenceit discharges. This downilow of wash water is maintained until all the residual juice has been displaced.

The exchanger bed is now ready for the teetering operation that is illustrated in Figs. and 14. This comprises, as has been previously explained, an upflow through the bed of wash liquid whereby solid phase impurities are washed out from the exchanger bed while size stratification of the particles is being established. Wash water enters from the wash water supply pipe 39, passes through the valve and continues through the by-pass connection 4i by way of the valve 42, leading into the central well 22 from Where it distributes itself over the space between the constriction plate i6 and the bottom of the cell. As indicated by the arrows, the wash liquid ilows upwardly and causes the normally settled exchanger bed to expand upwardly by forming a teeter bed of the depth T in which the particles or grains are kept vin suspension by suitable sustained upward ilow conditions, and at the same time range themselves in strata according to size, with the smallest particles in the top strata and the coarsest ones at the bottom. Under the flow conditions herein considered, there remains a depth t (see Fig. 14) of clear water between the top of the teeter bed and the point of overflow into the launder 49. During this upi'low operat- `ing phase the outlet valve e at the top of the cell is open to permit dischargev of spent teeter water, but all other valves at the lower end of the cell, and through which the water is not shown to ow, are closed. This sustained teeter condition due to, upilowing wash liquid is continued until the solid phase impurities will have been substantially iiushed out. It will also be noted that the perforated baille plate 5I during this phase has been floated upwardly to a point assaggi from reacting with the toeter bed and disturbing the uniform upfiow condition thereof. After the exchanger bed has thus been sumcientiy cleansed,.the particles must be allowed to settle back again, which is effected by permitting excess liquid to drain back through the bottom of the cell that is downward through the constriction plate I8. the central well 22, the radial pipe 30. valve I5 and again upwardly through the riser 33 from which it overows at an elevation that corresponds to the liquid level substantially to be maintained above the bed of settled particles in the cell. It will be noted that the baille plate 5| accordingly is carried from its upper (Fig. 10) position downward with the falling liquid level in Fig. 11 until it comes to rest again with the liquid level at the overflow elevation of the riser 33, when the exchanger grains have' come to rest and the cell is ready for the regeneration phase. During this draining operation, of course, the valve 53* remains open, but all other valves at the bottom end oi the cell through which the draining' liquid is not shown to flow, are closed.

According to Fig. 12 regenerant solution enters the unit from a supply pipe 35, flows through valve 36, and then passes throng the central vertical induction pipe 23 substantially in the same manner as described in conjunction with Figs. 8 and 9. At the bottom of the exchanger bed the spent regenerant liquor leaves the unit by way of the central well 422, the radial pipe 30, the valve 45, and by overflowing from the riser 32. This flow of regenerant solution through the bed is continued until the bed is considered suiilciently regenerated for re-use in the operating cycle, that is, for re-use in purification treatment of the sugar juice, shown in Figs. 8, 9, 12, 13 the automatic control of the liquid level in the cell may be allowed to function as set forth. During the teeter washing phase (see Fig. 10) however, this control is to be inoperative. In the subsequent wash water draining or solids settling phase (see Fig. 11), the automatic level control may again be allowed to function, and since it will then respond by admitting compressed air into the space above the liquid level, after the valve Silll has been closed, this will have the effect of expediting the downward discharge of the wash water until the normal operating level is again restored.

But before sugar juice can again be applied to the exchanger bed, the residual regenerant liquid in the bed must be displaced. This phase of the operating cycle is shown in Fig. 13 where wash water from pipe 39 passes by way of the central vertical induction pipe 23 and then downwardly through the exchanger bed substantially similar to the manner described in conjunction with the juice displacement phase `in Fig. 9, except that in Fig. 13 the outflowing liquid leaves the unit by way of the riser 32.

In view of the acidity of the juice and of the acid liquors respectively, to which the interior of the cell and its connections are exposed, their walls are made suitably acid-proof as by rubber coating. A conical acid-prooi' gasket 21 (see Fig. 5) is shown to surround the conical portion 21 of the feed induction pipe 23.

1; Anl exchanger cell comprising a receptacle adapted to hold a bed of granular exchanger material occupying a portion of the cell. whereby there is left a substantial free volume above the bed, a vertical feed conduit extending from the During the operating phase" asomar -4land interiorly in bottom ot the receptacle through said bed toa point above the top strata of the bed, controllable inlet meansl lfor passing 1iquid .tobe treated into and `.upwardlythrough `said reed conduit, said duit, means for vdiscliarging the liquid having passed'thrugh the. b ed ,from the ybottom of, the

receptacle substantially vat a rate at Ywhich itis fed whereby thebed-iskept substantially in s ubmergence, said `feed conduit being provided .with a valve seat at the upper'end thereof,oneway valve means provided yat the .upper end-of said feed conduit, and effectiveto admitliquid fed Yunder pressure to said receptacle, means forpassing an upward flow of wash water v throughrsaid bed whilek the supplyof pressure fed liquid to the feed conduitis shut off, which means comprise controllable inlet means for admitting the wash water underpressure at the bottom of the bed causing the level of the wash liquid to rise above said valve` seat and into said free volume of the receptacle, overflow means leading from the upper portion of the receptacle and determining the maximumlevel of ther wash water. and shut-off means for said overflow means.

2.v An exchanger, cell according to claim 1, in which the receptacle has a top closure portion, with the addition of control means for' maintaining` the leVelof the liquid in which `the, bed. is submerged between an upper and a lower :1imit, comprising a source of an auxiliary gaseous pressure medium, means operable to admit a quantity of said pressure medium into said receptacle to effect displacement of liquid from the receptacle through said discharge means when the level has unduly risen, and to shut off the admission of pressure medium when the level has been sutilciently lowered, and operable to release a quantity of said auxiliary pressure medium from the receptacle to allow the liquid level to risewhen the same has unduly dropped, and to shut off the release when the level has been suiiiciently raised.

3. An exchanger cell according to claim 1, in which the receptacle has a top closure portion, with the addition of automatic control means for maintaining the level of the liquid in which the bed is submerged between an upper and a lower limit, comprising a source of auxiliary gaseous pressure medium, valve means operable to admit a quantityof said pressure medium into said receptacle to displace liquid therefrom when the level has unduly risen, and to shut oli the admission of pressure medium when the'level has been suiiiciently lowered, and operable to release a quantity of said auxiliary pressure medium from the receptacle to allowpthe liquid level to rise when the same has unduly dropped, and to shut oi the release when the level has been sufliciently raised, float controlled devices actuated by said liquid level, and actuating means effective between said ldevices and said admittingand said releasing means for automatically maintaining said level within said limits.

4. An exchanger cell according to claim 1, with the addition of means for passing auxiliary water up through the feed conduit after the supply.

thereto of liquid to be treated has been shut off,

whereby there is eiected a downward displacement of the residual liquid in the bed -by said auxiliary water.

5. An exchanger cell according to claim 1, with the addition that said overflow means comprise an overflow launder disposed circumferentially tacle.

the top portion of the recep- V 6, .An-exchanger .cell accordinggtoclaim-f1, with upwardly due to said washl `water Vrising throughsaid receptacle. f

10 die' additin Otan annular baffle plate hai/inaper- An xchanger` cell according to with forations j and surrounding the Vupper terminal portion of lthe feed conduit, which baille plate ...is adaptedto iioat upon the lliquid in whichvv the exchanger bed is' submerged, and also adaptedto through'said receptacle. 8. An ,exchanger c ell according to claim 1, in which the receptacle hasa top closure portion,

float upwardlyy due `to saidwash waterjrising with the addition of `a cylindricalvmember supp ported from said top portion and extending therefromdownwardly into the vicinity of saidA valve means and substantially coaxially with said feed conduit. j Y

9. An exchangercell accordingv to claim 1,in which the receptaclehas a removable bottom portion. with the addition of constriction plate means for supporting the exchanger bed,said constriction 10. An exchanger cell according to claimfi,

in which the receptacle has a removable bottom portion provided with an opening, with the addition` of constriction plate means forl supporting the exchanger bed, said constriction plate means and said bottom portion forming between them a liquid collection and distributing space, spacing means provided on said bottom portion at points inwardly from the margin thereof and extending upwardly from said bottom portion kto support the constriction plate, a spider structure of radially extending ribs provided interiorly of and at the lower end of the receptacle, said constriction plate means being confined between said spacing means and said radial ribs, said spider structure having a central hub portion presenting aninterior conical seating face, said vertical feed conduit being provided with a conical portion adapted to engage said conical seating face, and means for holding in place and sealing saidinduction pipe with respect to said opening in the bottom portion.

11. An exchanger cell according to claim l, in which the receptacle has a removable botto-m portion provided with an opening, a spider structure of radially extending ribs provided interiorly of and'at the lower end of the receptacle, constric tion plate means for supporting and coniined between said bottom portion and said spider structure, said spider structure having a central hub portion presenting an interior conical seating face, said vertical feed conduitbeing provided 12. An exchanger cellaccording toclaiml, in' which the receptacle rhas a removable bottomportion formed "with'a' centralv well portion and a bottom opening therein and also formed with liquid collecting channels extending radially from said well portion, a spider structure of radially extending ribs provided interiorly oi.' and at 'the lower end of the receptacle, constriction plate means for supporting said bed and coniined between said .bottom portion and said spider structure, said spider structure having a centra1 hub portion presenting an interior conical seating face, said vertical feed conduit being provided with a corresponding conical portion adapted to engage said conical seating iace when the feed conduit is introduced from below through said hub portion, and means i'or holding in place and sealing said feed vpipe. with respect to said opening in the bottom portion.

13. An exchanger cell according to claim 1, in which the receptacle has a removable bottom portion provided with an opening, a spider structure of radially extending ribs provided interiorly of and at the lower end of the receptacle, constriction plate means for supporting said bed and conilned between said bottom portion and said spider structure, said spider structure having a central hub portion adapted to have substantial sealing engagement with said vertical feed conduit when the same is introduced from below through said hub portion, and means for holding in place and sealing said feed pipe with respect to said opening in bottom portion.

14. An exchanger cell according to claim 1, in which the receptacle has a removable bottom portion provided with a central well portion having an opening in the bottom thereof, and also provided with distributing channels extending radially from said well portion, a spider structure of radially extending ribs provided interiorly of and at the lower end of the receptacle, constriction plate means for supporting said bed and confined between said bottom portion and said spider structure, said spider structure having a central hub portion adapted to have sealing engagement with said feed conduit when the same is introduced from below through said hub portion, and means for holding in place and sealing said feed conduit with respect to said opening.

15. An exchanger cell according to claim l, in which the receptacle has a removable bottom portion provided with a central well portion having an opening in the bottom thereof, and also provided with distributing channels extending radially from said well portion, at least one cylindrical spacer baille concentric with said well portion and provided on said bottom portion so as to traverse said channels, constriction plate means supported by said spacer baille for supporting the bed, a spider structure of radially extending ribs provided interiorly of and at the lower end of the receptacle, said spider structure having a central hub portion adapted to have sealing engagement with saidrfeed pipe when the same is introduced from below through said hub portion, and means for holding in place andr sealing said feed conduit with respect to said aperture in the bottom portion.

16. A liquid treatment cell comprising a closed receptacle adapted to hold a bed of granular material, means for feeding liquid to said bed for passage downwardly therethrough, means for discharging liquid from said bed substantially at a rate at which it is fed, whereby the bed is adapted to be kept insubmergence, and means assaggi for controlling the levely of the liquid passing downwardly through the bed so as to maintain Isaid level between an upper and a lower limit, comprising a source of an auxiliary gaseous pressure medium, pressure admitting means operable to admit a quantity of said pressure medium into said receptacle to displace liquid from the receptacle through said liquid discharge means to lower the liquid level-when the same has unduly risen, and to shut off the admission of pressure medium to the receptacle when th level has been sumciently lowered, and press means operable to release a quantity of auxiliary pressure medium from said receptacle to allow the liquid level to rise when the same has unduly dropped, and to shut oil the release when the level has been sumciently raised.

17. A liquid treatment cell according to claim 16, with the addition of automatic means for controlling the liquid level, which means are responsive to changes of said liquid level, comprising a float-controlled device actuated by said liquid level, and actuating means effective between said device and the pressure admitting means for admitting said pressure medium to lower the liq uid level, and for shutting oi said pressure medlum when the level has been sulciently lowered, and comprising a second float-controlled device actuated by said liquid level, and actuating means effective between said second device and the pressure releasing means for releasing said pressure medium from the receptacle to raise the liquid level, as well as for shutting off the release when the level has been sufficiently raised.

` 18.'A liquid treatment cell according to claim 16, with the addition of automatic means for controlling the liquid level, which means are responsive to changes of the level, comprising a photoelectric device actuated by a light beam adapted to be affected by said liquid with the rise and fall thereof, electric impulse means effective between said device and the pressure admitting means for admitting said pressure medium to lower the liquid level as well as for shutting oif said pressure medium when the level has been sumciently lowered, a second photo-electric device actuated by a light beam adapted to be affected by said liquid with the fall and rise thereof, electric impulse means eective between said last mentioned device and the pressure releasing means for releasing pressure medium from said receptacle to raise the liquid level as well as for shutting oi the release when the level has been sufficiently raised.

19. In the treatment of sugar bearing liquids the method of operating an exchanger bed contained in a closed tank having substantial freeboard space above the bed, which comprises passing the liquid downwardly through the bed against a ilow resistance, and maintaining the bed substantially submerged by controlling the pressure of a gaseous medium above the bed and said flow resistance relative to one another in a manner to maintain the liquid level substantially at the top strata of the bed.

20. The method according to claim 19, in which said liquid level is controlled by admitting additional gaseous medium to, or releasing a portion of the coniined medium from said tank.

RALPH W. SHAFOR e releasing' 

